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C:\Users\kp\Desktop\HTRI-1.htri Output Summary Page 1 Released to the following HTRI Member Company: SYNERGY KALPAN Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental Baffles See Data Check Messages Report for Informative Messages. See Runtime Message Report for Warning Messages. Process Conditions Hot Shellside Cold Tubeside Fluid name Brine R404A Flow rate (kg/s) 0.1604 0.2100 Inlet/Outlet Y (Wt. frac vap.) 0.000 0.000 0.000 0.000 Inlet/Outlet T (Deg C) -20.00 -26.00 -33.00 -23.00 Inlet P/Avg (kPa) 0.000 0.000 0.000 0.000 dP/Allow. (kPa) 0.191 0.000 0.228 0.000 Fouling (m2-K/W) 0.000789 0.000690 Exchanger Performance Shell h (W/m2-K) 501.74 Actual U (W/m2-K) 118.11 Tube h (W/m2-K) 250.99 Required U (W/m2-K) 561.25 Hot regime (--) Sens. Liquid Duty (MegaWatts) 0.0027 Cold regime (--) Sens. Liquid Area (m2) 4.281 EMTD (Deg C) 1.1 Overdesign (%) -78.96 Shell Geometry Baffle Geometry TEMA type (--) BEM Baffle type (--) Single-Seg. Shell ID (mm) 203.200 Baffle cut (Pct Dia.) 25.00 Series (--) 1 Baffle orientation (--) Perpend. Parallel (--) 1 Central spacing (mm) 101.600 Orientation (deg) 0.00 Crosspasses (--) 15 Tube Geometry Nozzles Tube type (--) Plain Shell inlet (mm) 26.645 Tube OD (mm) 19.050 Shell outlet (mm) 26.645 Length (m) 1.829 Inlet height (mm) 19.065 Pitch ratio (--) 1.2500 Outlet height (mm) 19.065 Layout (deg) 30 Tube inlet (mm) 26.645 Tubecount (--) 40 Tube outlet (mm) 26.645 Tube Pass (--) 4 Thermal Resistance, % Velocities, m/s Flow Fractions Shell 23.53 Shellside 2.669e-2 A 0.014 Tube 56.92 Tubeside 8.702e-2 B 0.682 Fouling 19.20 Crossflow 2.628e-2 C 0.048 Metal 0.353 Window 2.639e-2 E 0.257 F 0.000
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  • C:\Users\kp\Desktop\HTRI-1.htri

    Output Summary Page 1Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesSee Data Check Messages Report for Informative Messages.See Runtime Message Report for Warning Messages.

    Process Conditions Hot Shellside Cold TubesideFluid name Brine R404A Flow rate (kg/s) 0.1604 0.2100Inlet/Outlet Y (Wt. frac vap.) 0.000 0.000 0.000 0.000Inlet/Outlet T (Deg C) -20.00 -26.00 -33.00 -23.00Inlet P/Avg (kPa) 0.000 0.000 0.000 0.000dP/Allow. (kPa) 0.191 0.000 0.228 0.000Fouling (m2-K/W) 0.000789 0.000690

    Exchanger PerformanceShell h (W/m2-K) 501.74 Actual U (W/m2-K) 118.11Tube h (W/m2-K) 250.99 Required U (W/m2-K) 561.25Hot regime (--) Sens. Liquid Duty (MegaWatts) 0.0027Cold regime (--) Sens. Liquid Area (m2) 4.281EMTD (Deg C) 1.1 Overdesign (%) -78.96

    Shell Geometry Baffle GeometryTEMA type (--) BEM Baffle type (--) Single-Seg.Shell ID (mm) 203.200 Baffle cut (Pct Dia.) 25.00Series (--) 1 Baffle orientation (--) Perpend.Parallel (--) 1 Central spacing (mm) 101.600Orientation (deg) 0.00 Crosspasses (--) 15

    Tube Geometry NozzlesTube type (--) Plain Shell inlet (mm) 26.645Tube OD (mm) 19.050 Shell outlet (mm) 26.645Length (m) 1.829 Inlet height (mm) 19.065Pitch ratio (--) 1.2500 Outlet height (mm) 19.065Layout (deg) 30 Tube inlet (mm) 26.645Tubecount (--) 40 Tube outlet (mm) 26.645Tube Pass (--) 4

    Thermal Resistance, % Velocities, m/s Flow FractionsShell 23.53 Shellside 2.669e-2 A 0.014Tube 56.92 Tubeside 8.702e-2 B 0.682Fouling 19.20 Crossflow 2.628e-2 C 0.048Metal 0.353 Window 2.639e-2 E 0.257

    F 0.000

  • C:\Users\kp\Desktop\HTRI-1.htri

    Run Log Page 2Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesBeginning Run Running Xist Unit 1, 100Run Converged. Solution Reached.Total runtime: 00:00:11

  • C:\Users\kp\Desktop\HTRI-1.htri

    Data Check Messages Page 3Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesUnit ID 100

    There are no messages for the current message level setting.

  • C:\Users\kp\Desktop\HTRI-1.htri

    Runtime Messages Page 4Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesUnit ID 100 - WARNING MESSAGES (CALCULATIONS CONTINUE)

    The maximum process temperature is outside the correlational range of the automatic tube materialdata bank. The tube metal properties were calculated at the temperature limit. For tube metalnumber 1 the temperature limit is 21.11 C. Temperature limits are available in the HTRI XchangerSuite online help file.

    The estimated tube count for this shell is 30. A large variation from the expected tube count mayindicate that program has used different clearances (such as bundle-to-shell clearance andheights-under-nozzles) than those expected. Although the specified number of tubes has beenused to calculate the available heat transfer area, discrepancies in exchanger clearances can resultin inaccurate pressure drop and heat transfer calculations.

    An internal temperature cross exists in the exchanger. The program handles the reverse heat flowproperly in the calculations, but you may want to consider changing the terminal process conditionsto avoid the internal temperature cross.

  • C:\Users\kp\Desktop\HTRI-1.htri

    Final Results Page 5Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesProcess Data Hot Shellside Cold Tubeside

    Fluid name Brine R404A Fluid condition Sens. Liquid Sens. LiquidTotal flow rate (kg/s) 0.1604 0.2100Weight fraction vapor, In/Out (--) 0.000 0.000 0.000 0.000Temperature, In/Out (Deg C) -20.00 -26.00 -33.00 -23.00Temperature, Average/Skin (Deg C) -23.0 -24.05 -28.0 -24.45Wall temperature, Min/Max (Deg C) -28.23 -21.24 -28.25 -21.25Pressure, In/Average (kPa) 0.000 0.000 0.000 0.000Pressure drop, Total/Allowed (kPa) 0.191 0.228Velocity, Mid/Max allow (m/s) 2.669e-2 8.702e-2Mole fraction inert (--)Average film coef. (W/m2-K) 501.74 250.99Heat transfer safety factor (--) 1.000 1.000Fouling resistance (m2-K/W) 0.000789 0.000690

    Overall Performance DataOverall coef., Reqd/Clean/Actual (W/m2-K) 561.25 / 146.16 / 118.11Heat duty, Calculated/Specified (MegaWatts) 0.0027 /Effective overall temperature difference (Deg C) 1.1EMTD = (MTD) * (DELTA) * (F/G/H) (Deg C) 1.97 * 0.5737 * 1.0000

    See Runtime Messages Report for warnings.

    Exchanger Fluid VolumesApproximate shellside (L) 37.0Approximate tubeside (L) 32.6

    Shell Construction InformationTEMA shell type BEM Shell ID (mm) 203.200Shells Series 1 Parallel 1 Total area (m2) 4.378Passes Shell 1 Tube 4 Eff. area (m2/shell) 4.281Shell orientation angle (deg) 0.00Impingement present NoPairs seal strips 1 Passlane seal rods (mm) 0.000 No. 0Shell expansion joint No Rear head support plate NoWeight estimation Wet/Dry/Bundle 295.76 / 226.19 / 65.80 (kg/shell)

    Baffle InformationType Perpend. Single-Seg. Baffle cut (% dia) 25.00Crosspasses/shellpass 15 No. (Pct Area) (mm) to C.LCentral spacing (mm) 101.600 1 22.34 50.800Inlet spacing (mm) 233.771 2 0.00 0.000Outlet spacing (mm) 233.771Baffle thickness (mm) 3.175

    Tube InformationTube type Plain Tubecount per shell 40Overall length (m) 1.829 Pct tubes removed (both) 5Effective length (m) 1.788 Outside diameter (mm) 19.050Total tubesheet (mm) 40.640 Wall thickness (mm) 1.650Area ratio (out/in) 1.2095 Pitch (mm) 23.8125 Ratio 1.2500Tube metal Carbon steel Tube pattern (deg) 30

    1.829 m

    203.200 mm

  • C:\Users\kp\Desktop\HTRI-1.htri

    Final Results Page 6Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesShellside Performance

    Nom vel, X-flow/window 2.628e-2 / 2.639e-2

    Flow fractions for heat transfer 0.700 A=0.0142 B=0.6817 C=0.0476 E=0.2566 F=0.0000

    Shellside Heat Transfer CorrectionsTotal Beta Gamma End Fin0.920 0.920 1.000 0.948 1.000

    Pressure Drops (Percent of Total)Cross Window Ends Nozzle Shell Tube33.38 11.47 6.83 Inlet 24.03 27.09

    MOMENTUM 0.00 Outlet 24.29 17.67Two-Phase Parameters

    Method Inlet Center Outlet Mix F

    H. T. Parameters Shell TubeOverall wall correction 0.996 0.997Midpoint Prandtl no. 75.24 3.61Midpoint Reynolds no. 46 6942Bundle inlet Reynolds no. 24 6316Bundle outlet Reynolds no. 21 7079Fouling layer (mm)

    Thermal ResistanceShell Tube Fouling Metal Over Des

    23.53 56.92 19.20 0.353 -78.96Total fouling resistance 0.00162Differential resistance -0.00668

    Shell Nozzles LiquidInlet at channel end-No Inlet Outlet OutletNumber at each position 1 1 0Diameter (mm) 26.645 26.645Velocity (m/s) 0.22 0.22Pressure drop (kPa) 0.046 0.046Height under nozzle (mm) 19.065 19.065Nozzle R-V-SQ (kg/m-s2) 64.01 63.91Shell ent. (kg/m-s2) 7.14 7.13

    Inlet Outlet LiquidTube Nozzle RADIAL RADIAL Outlet

    Diameter (mm) 26.645 26.645Velocity (m/s) 0.30 0.31Pressure drop (kPa) 0.062 0.040Nozzle R-V-SQ (kg/m-s2) 112.23 115.00

    Annular Distributor Inlet OutletLength (mm)Height (mm)Slot area (mm2)

    Diametral Clearances (mm)Baffle-to-shell Bundle-to-shell Tube-to-baffle

    3.1750 13.8426 0.7938

  • C:\Users\kp\Desktop\HTRI-1.htri

    Supplementary Results Page 7Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesExternally Enhanced Tube Geometry Internally Enhanced Tube Geometry

    Type Plain Type NoneFin density (fin/meter) Thickness (mm)Fin height (mm) Pitch (L/D)Fin thickness (mm)Root diameter (mm)Area/length (m2/m)

    Mean Metal TemperaturesMean shell temperature -23.55 (C)

    Mean tube metal temperature in each tubepass, (C)Tube Pass Inside Outside Radial

    1 -25.70 -25.68 -25.692 -24.10 -24.10 -24.103 -23.85 -23.84 -23.854 -23.36 -23.36 -23.36

  • C:\Users\kp\Desktop\HTRI-1.htri

    Shellside Incremental Monitor Page 8Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesShellside Flow Region 1 0.1604 kg/sPoint number (--) 1 2 3 4 5Shell pass (--) 1 1 1 1 1Length from tube inlet (mm) 1788.34 1671.46 1503.77 1402.17 1300.57Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -20.00 -20.76 -21.76 -22.23 -22.64Skin temperature (C) -21.82 -22.58 -22.84 -23.28MTD (C) 4.4 3.2 2.9 2.5Delta MTD correction (--) 0.986 0.908 0.890 0.083Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 0.046 6.178e-3 6.337e-3 6.376e-3 6.446e-3Friction loss (kPa) 6.178e-3 6.337e-3 6.376e-3 6.446e-3Static head loss (kPa) 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000Area (m2) 0.560 0.243 0.243 0.243Cumulative area (m2) 0.560 0.803 1.046 1.289Duty (MegaWatts) 6.665e-4 2.200e-4 2.000e-4 1.653e-4Cumulative duty (MegaWatts) 6.665e-4 8.864e-4 0.0011 0.0013Heat flux (W/m2) 1190.95 904.35 822.14 679.66Calculated heat flux (W/m2) 499.80 349.49 311.63 23.98Critical heat flux (W/m2)Overall U (W/m2-K) 116.67 120.42 119.91 118.94Shellside h (W/m2-K) 439.14 526.78 527.20 527.93Sensible liquid h (W/m2-K) 439.14 526.78 527.20 527.93Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00Local Reynolds (--) 24 29 48 48 47Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 24 29 48 48 47Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 64.85 66.49 69.46 70.31 71.79Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000Condensate regime (--) Sens Liq Sens Liq Sens Liq Sens LiqBoiling regime (--)Boiling mechanism (--)

  • C:\Users\kp\Desktop\HTRI-1.htri

    Shellside Incremental Monitor Page 9Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesShellside Flow Region 1Point number (--) 6 7 8 9 10Shell pass (--) 1 1 1 1 1Length from tube inlet (mm) 1198.97 1097.37 995.771 894.171 792.571Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -22.99 -23.32 -23.61 -23.89 -24.15Skin temperature (C) -23.44 -23.83 -23.96 -24.31 -24.41MTD (C) 2.4 2.6 2.5 2.2 2.2Delta MTD correction (--) 0.671 0.286 0.189 0.239 0.171Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 6.470e-3 6.533e-3 6.550e-3 6.608e-3 6.620e-3Friction loss (kPa) 6.470e-3 6.533e-3 6.550e-3 6.608e-3 6.620e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Area (m2) 0.243 0.243 0.243 0.243 0.243Cumulative area (m2) 1.532 1.776 2.019 2.262 2.505Duty (MegaWatts) 1.563e-4 1.370e-4 1.329e-4 1.183e-4 1.176e-4Cumulative duty (MegaWatts) 0.0014 0.0015 0.0017 0.0018 0.0019Heat flux (W/m2) 642.45 563.43 546.52 486.37 483.48Calculated heat flux (W/m2) 183.48 68.17 43.60 48.81 34.57Critical heat flux (W/m2)Overall U (W/m2-K) 118.62 118.51 118.27 118.26 118.10Shellside h (W/m2-K) 528.19 528.81 528.99 529.54 529.66Sensible liquid h (W/m2-K) 528.19 528.81 528.99 529.54 529.66Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 47 47 46 46 46Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 47 47 46 46 46Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 72.32 73.64 74.02 75.24 75.51Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling regime (--)Boiling mechanism (--)

  • C:\Users\kp\Desktop\HTRI-1.htri

    Shellside Incremental Monitor Page 10Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesShellside Flow Region 1Point number (--) 11 12 13 14 15Shell pass (--) 1 1 1 1 1Length from tube inlet (mm) 690.971 589.371 487.771 386.171 284.571Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -24.39 -24.62 -24.85 -25.06 -25.31Skin temperature (C) -24.75 -24.82 -25.15 -25.22 -25.57MTD (C) 2.0 2.1 4.2 4.3 4.3Delta MTD correction (--) 0.049 0.153 0.050 0.035 0.050Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 6.675e-3 6.683e-3 6.738e-3 6.744e-3 6.803e-3Friction loss (kPa) 6.675e-3 6.683e-3 6.738e-3 6.744e-3 6.803e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Area (m2) 0.243 0.243 0.243 0.243 0.243Cumulative area (m2) 2.749 2.992 3.235 3.478 3.721Duty (MegaWatts) 1.047e-4 1.072e-4 1.038e-4 1.076e-4 1.112e-4Cumulative duty (MegaWatts) 0.0020 0.0021 0.0022 0.0023 0.0024Heat flux (W/m2) 430.36 440.74 426.77 442.48 457.13Calculated heat flux (W/m2) 8.69 28.06 8.69 6.34 9.10Critical heat flux (W/m2)Overall U (W/m2-K) 117.83 118.06 118.48 118.82 119.93Shellside h (W/m2-K) 530.18 530.26 530.76 530.82 531.35Sensible liquid h (W/m2-K) 530.18 530.26 530.76 530.82 531.35Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 45 45 45 45 44Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 45 45 45 45 44Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 76.67 76.85 78.01 78.16 79.40Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling regime (--)Boiling mechanism (--)

  • C:\Users\kp\Desktop\HTRI-1.htri

    Shellside Incremental Monitor Page 11Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesShellside Flow Region 1Point number (--) 16 17Shell pass (--) 1 1Length from tube inlet (mm) 116.885 0.000Mass fraction vapor (--) 0.0000 0.0000Bulk temperature (C) -25.69 -26.00Skin temperature (C) -25.70MTD (C) 4.6Delta MTD correction (--) 0.036Pressure (kPa) 0.000 0.000Pressure drop (kPa) 6.857e-3 0.046Friction loss (kPa) 6.857e-3Static head loss (kPa) 0.000Momentum loss (kPa) 0.000Area (m2) 0.560Cumulative area (m2) 4.281Duty (MegaWatts) 2.659e-4Cumulative duty (MegaWatts) 0.0027Heat flux (W/m2) 475.13Calculated heat flux (W/m2) 6.88Critical heat flux (W/m2)Overall U (W/m2-K) 115.77Shellside h (W/m2-K) 444.36Sensible liquid h (W/m2-K) 444.36Sensible vapor h (W/m2-K) 0.00Condensate film h (W/m2-K) 0.00Vapor phase h (W/m2-K) 0.00Nucleate boiling h (W/m2-K) 0.00Conv. boiling h (W/m2-K) 0.00Film boiling h (W/m2-K) 0.00Boiling thin film h (W/m2-K) 0.00Natural convective h (W/m2-K) 0.00Local Reynolds (--) 26 21Vapor Reynolds (--) 0 0Liquid Reynolds (--) 26 21Vapor Prandtl (--) 0.00 0.00Liquid Prandtl (--) 79.67 81.20Flow regime param. (--) 0.0000Condensate regime (--) Sens LiqBoiling regime (--)Boiling mechanism (--)

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 12Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 1 2 3 4 5Tube Pass (--) 1 1 1 1 1Length from tube inlet (mm) 0.000 116.885 284.571 386.171 487.771Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -33.00 -32.50 -31.79 -31.37 -30.98Skin temperature (C) -28.89 -28.20 -27.85 -27.53MTD (C) 6.8 6.5 6.3 6.1Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 0.062 3.008e-3 1.202e-3 1.202e-3 1.202e-3Enhanced pressure drop mult (--)Friction loss (kPa) 3.008e-3 1.202e-3 1.202e-3 1.202e-3Static head loss (kPa) 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.539e-2 8.554e-2 8.562e-2 8.571e-2Average velocity (m/s) 8.539e-2 8.553e-2 8.562e-2 8.570e-2Area (m2) 0.140 0.061 0.061 0.061Cumulative area (m2) 0.140 0.201 0.262 0.322Duty (MegaWatts) 2.700e-4 1.130e-4 1.088e-4 1.050e-4Cumulative duty (MegaWatts) 2.700e-4 3.830e-4 4.918e-4 5.967e-4Heat flux (W/m2) 1929.56 1858.88 1789.06 1726.33Calculated heat flux (W/m2) 821.05 791.04 761.34 734.67Critical heat flux (W/m2) 0.00 0.00 0.00 0.00Overall U (W/m2-K) 121.15 122.32 120.97 120.02Tubeside h (W/m2-K) 275.58 266.73 261.50 257.93Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 275.58 266.73 261.50 257.93Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00Local Reynolds (--) 6316 6319 6375 6408 6439Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 6316 6319 6375 6408 6439Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.78 3.77 3.76 3.75 3.74Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 13Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 6 7 8 9 10Tube Pass (--) 1 1 1 1 1Length from tube inlet (mm) 589.371 690.971 792.571 894.171 995.771Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -30.60 -30.23 -29.87 -29.51 -29.17Skin temperature (C) -27.22 -26.91 -26.62 -26.29 -26.02MTD (C) 6.0 5.8 5.7 5.6 5.5Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 1.201e-3 1.201e-3 1.201e-3 1.201e-3 1.200e-3Enhanced pressure drop mult (--)Friction loss (kPa) 1.201e-3 1.201e-3 1.201e-3 1.201e-3 1.200e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.579e-2 8.587e-2 8.594e-2 8.602e-2 8.609e-2Average velocity (m/s) 8.578e-2 8.586e-2 8.593e-2 8.601e-2 8.608e-2Area (m2) 0.061 0.061 0.061 0.061 0.061Cumulative area (m2) 0.383 0.444 0.505 0.566 0.626Duty (MegaWatts) 1.016e-4 9.877e-5 9.589e-5 9.488e-5 9.237e-5Cumulative duty (MegaWatts) 6.983e-4 7.971e-4 8.930e-4 9.879e-4 0.0011Heat flux (W/m2) 1670.74 1624.36 1576.97 1560.44 1519.16Calculated heat flux (W/m2) 711.03 691.34 671.18 664.18 646.62Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 119.25 118.58 118.11 117.90 117.72Tubeside h (W/m2-K) 255.08 252.60 250.90 250.20 249.55Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 255.08 252.60 250.90 250.20 249.55Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 6469 6499 6528 6556 6583Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 6469 6499 6528 6556 6583Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.73 3.72 3.71 3.71 3.70Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 14Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 11 12 13 14 15Tube Pass (--) 1 1 1 1 1Length from tube inlet (mm) 1097.37 1198.97 1300.57 1402.17 1503.77Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -28.82 -28.49 -28.15 -27.81 -27.46Skin temperature (C) -25.65 -25.39 -24.96 -24.69 -24.13MTD (C) 5.6 5.4 5.6 5.5 5.8Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 1.200e-3 1.200e-3 1.199e-3 1.199e-3 1.198e-3Enhanced pressure drop mult (--)Friction loss (kPa) 1.200e-3 1.200e-3 1.199e-3 1.199e-3 1.198e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.616e-2 8.624e-2 8.631e-2 8.638e-2 8.645e-2Average velocity (m/s) 8.615e-2 8.622e-2 8.629e-2 8.637e-2 8.644e-2Area (m2) 0.061 0.061 0.061 0.061 0.061Cumulative area (m2) 0.687 0.748 0.809 0.870 0.930Duty (MegaWatts) 9.305e-5 9.068e-5 9.348e-5 9.112e-5 9.760e-5Cumulative duty (MegaWatts) 0.0012 0.0013 0.0014 0.0014 0.0015Heat flux (W/m2) 1530.30 1491.25 1537.45 1498.55 1605.16Calculated heat flux (W/m2) 651.39 634.78 654.47 637.92 683.30Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 117.63 117.51 117.55 117.40 117.57Tubeside h (W/m2-K) 249.35 248.93 249.23 248.71 249.53Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 249.35 248.93 249.23 248.71 249.53Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 6611 6638 6665 6692 6720Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 6611 6638 6665 6692 6720Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.69 3.69 3.68 3.67 3.67Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 15Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 16 17 18 19 20Tube Pass (--) 1 2 2 2 2Length from tube inlet (mm) 1671.46 1671.46 1503.77 1402.17 1300.57Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -26.89 -26.13 -25.62 -25.40 -25.21Skin temperature (C) -23.77 -23.33 -23.46 -23.56 -23.77MTD (C) 5.6 5.3 3.8 3.2 2.5Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 3.014e-3 3.015e-3 1.199e-3 1.200e-3 1.200e-3Enhanced pressure drop mult (--)Friction loss (kPa) 3.014e-3 3.015e-3 1.199e-3 1.200e-3 1.200e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.657e-2 8.672e-2 8.683e-2 8.688e-2 8.692e-2Average velocity (m/s) 8.656e-2 8.672e-2 8.683e-2 8.688e-2 8.691e-2Area (m2) 0.140 0.140 0.061 0.061 0.061Cumulative area (m2) 1.070 1.210 1.271 1.332 1.393Duty (MegaWatts) 2.100e-4 2.073e-4 6.741e-5 5.611e-5 4.332e-5Cumulative duty (MegaWatts) 0.0018 0.0020 0.0020 0.0021 0.0021Heat flux (W/m2) 1501.23 1481.64 1108.59 922.75 712.41Calculated heat flux (W/m2) 639.07 630.76 472.06 392.96 303.46Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 114.30 119.40 124.61 123.39 122.29Tubeside h (W/m2-K) 248.88 274.79 265.46 260.80 256.64Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 248.88 274.79 265.46 260.80 256.64Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 6765 6827 6868 6886 6901Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 6765 6827 6868 6886 6901Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.65 3.64 3.63 3.63 3.62Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 16Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 21 22 23 24 25Tube Pass (--) 2 2 2 2 2Length from tube inlet (mm) 1198.97 1097.37 995.771 894.171 792.571Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -25.07 -24.95 -24.86 -24.80 -24.75Skin temperature (C) -23.82 -24.05 -24.08 -24.32 -24.34MTD (C) 2.1 1.6 1.3 8.148e-1 6.979e-1Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 1.200e-3 1.201e-3 1.201e-3 1.202e-3 1.202e-3Enhanced pressure drop mult (--)Friction loss (kPa) 1.200e-3 1.201e-3 1.201e-3 1.202e-3 1.202e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.695e-2 8.697e-2 8.699e-2 8.701e-2 8.701e-2Average velocity (m/s) 8.695e-2 8.697e-2 8.699e-2 8.700e-2 8.701e-2Area (m2) 0.061 0.061 0.061 0.061 0.061Cumulative area (m2) 1.453 1.514 1.575 1.636 1.697Duty (MegaWatts) 3.677e-5 2.635e-5 2.246e-5 1.356e-5 1.157e-5Cumulative duty (MegaWatts) 0.0022 0.0022 0.0022 0.0022 0.0022Heat flux (W/m2) 604.70 433.30 369.32 223.00 190.21Calculated heat flux (W/m2) 257.59 184.66 157.40 95.14 81.15Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 121.40 120.56 119.93 119.34 118.83Tubeside h (W/m2-K) 253.38 250.24 247.99 245.80 244.00Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 253.38 250.24 247.99 245.80 244.00Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 6913 6922 6929 6934 6938Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 6913 6922 6929 6934 6938Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.62 3.62 3.62 3.61 3.61Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 17Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 26 27 28 29 30Tube Pass (--) 2 2 2 2 2Length from tube inlet (mm) 690.971 589.371 487.771 386.171 284.571Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -24.72 -24.71 -24.70 -24.70 -24.71Skin temperature (C) -24.59 -24.59 -24.86 -24.85 -25.14MTD (C) 2.300e-1 2.002e-1 -2.56e-1 -2.51e-1 -7.27e-1Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 1.202e-3 1.202e-3 1.203e-3 1.203e-3 1.203e-3Enhanced pressure drop mult (--)Friction loss (kPa) 1.202e-3 1.202e-3 1.203e-3 1.203e-3 1.203e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.702e-2 8.702e-2 8.702e-2 8.702e-2 8.702e-2Average velocity (m/s) 8.702e-2 8.702e-2 8.702e-2 8.702e-2 8.702e-2Area (m2) 0.061 0.061 0.061 0.061 0.061Cumulative area (m2) 1.757 1.818 1.879 1.940 2.001Duty (MegaWatts) 3.577e-6 3.131e-6 -1.19e-7 -1.17e-7 -3.43e-7Cumulative duty (MegaWatts) 0.0022 0.0022 0.0022 0.0022 0.0022Heat flux (W/m2) 58.82 51.49 -1.96 -1.92 -5.64Calculated heat flux (W/m2) 25.24 22.08 -3.93 -3.85 -11.26Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 117.43 117.40 117.35 117.22 118.13Tubeside h (W/m2-K) 239.06 238.98 238.70 238.27 241.28Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 239.06 238.98 238.70 238.27 241.28Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 6940 6941 6942 6942 6942Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 6940 6941 6942 6942 6942Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.61 3.61 3.61 3.61 3.61Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 18Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 31 32 33 34 35Tube Pass (--) 2 3 3 3 3Length from tube inlet (mm) 116.885 116.885 284.571 386.171 487.771Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -24.71 -24.71 -24.71 -24.71 -24.71Skin temperature (C) -25.11 -25.09 -25.13 -24.85 -24.86MTD (C) -7.14e-1 -7.17e-1 -7.25e-1 -2.47e-1 -2.51e-1Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 3.010e-3 3.010e-3 1.203e-3 1.203e-3 1.203e-3Enhanced pressure drop mult (--)Friction loss (kPa) 3.010e-3 3.010e-3 1.203e-3 1.203e-3 1.203e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.702e-2 8.702e-2 8.702e-2 8.702e-2 8.702e-2Average velocity (m/s) 8.702e-2 8.702e-2 8.702e-2 8.702e-2 8.702e-2Area (m2) 0.140 0.140 0.061 0.061 0.061Cumulative area (m2) 2.141 2.280 2.341 2.402 2.463Duty (MegaWatts) -7.32e-7 -7.67e-7 -3.53e-7 -1.18e-7 -1.19e-7Cumulative duty (MegaWatts) 0.0022 0.0022 0.0022 0.0022 0.0022Heat flux (W/m2) -5.23 -5.48 -5.80 -1.94 -1.96Calculated heat flux (W/m2) -10.43 -10.93 -11.57 -3.88 -3.92Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 111.48 116.26 121.89 119.83 119.24Tubeside h (W/m2-K) 240.79 259.87 254.54 247.32 245.24Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 240.79 259.87 254.54 247.32 245.24Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 6942 6942 6942 6942 6942Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 6942 6942 6942 6942 6942Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.61 3.61 3.61 3.61 3.61Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 19Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 36 37 38 39 40Tube Pass (--) 3 3 3 3 3Length from tube inlet (mm) 589.371 690.971 792.571 894.171 995.771Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -24.71 -24.70 -24.67 -24.63 -24.58Skin temperature (C) -24.58 -24.58 -24.29 -24.26 -23.93MTD (C) 2.004e-1 1.926e-1 6.393e-1 6.217e-1 1.1Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 1.202e-3 1.202e-3 1.202e-3 1.202e-3 1.201e-3Enhanced pressure drop mult (--)Friction loss (kPa) 1.202e-3 1.202e-3 1.202e-3 1.202e-3 1.201e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.702e-2 8.703e-2 8.703e-2 8.704e-2 8.705e-2Average velocity (m/s) 8.702e-2 8.703e-2 8.703e-2 8.704e-2 8.705e-2Area (m2) 0.061 0.061 0.061 0.061 0.061Cumulative area (m2) 2.524 2.584 2.645 2.706 2.767Duty (MegaWatts) 3.193e-6 3.045e-6 1.063e-5 1.035e-5 1.833e-5Cumulative duty (MegaWatts) 0.0022 0.0023 0.0023 0.0023 0.0023Heat flux (W/m2) 52.51 50.08 174.84 170.16 301.45Calculated heat flux (W/m2) 22.49 21.46 74.54 72.55 128.41Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 118.49 118.12 118.53 118.73 118.97Tubeside h (W/m2-K) 242.72 241.46 242.96 243.67 244.63Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 242.72 241.46 242.96 243.67 244.63Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 6942 6943 6945 6948 6952Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 6942 6943 6945 6948 6952Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.61 3.61 3.61 3.61 3.61Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 20Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 41 42 43 44 45Tube Pass (--) 3 3 3 3 3Length from tube inlet (mm) 1097.37 1198.97 1300.57 1402.17 1503.77Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -24.51 -24.43 -24.34 -24.22 -24.09Skin temperature (C) -23.89 -23.50 -23.42 -22.97 -22.82MTD (C) 1.1 1.6 1.5 2.1 2.2Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 1.201e-3 1.201e-3 1.200e-3 1.200e-3 1.199e-3Enhanced pressure drop mult (--)Friction loss (kPa) 1.201e-3 1.201e-3 1.200e-3 1.200e-3 1.199e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.706e-2 8.708e-2 8.710e-2 8.713e-2 8.716e-2Average velocity (m/s) 8.706e-2 8.708e-2 8.710e-2 8.713e-2 8.716e-2Area (m2) 0.061 0.061 0.061 0.061 0.061Cumulative area (m2) 2.828 2.888 2.949 3.010 3.071Duty (MegaWatts) 1.788e-5 2.667e-5 2.616e-5 3.629e-5 3.666e-5Cumulative duty (MegaWatts) 0.0023 0.0023 0.0024 0.0024 0.0024Heat flux (W/m2) 294.01 438.57 430.17 596.91 602.90Calculated heat flux (W/m2) 125.25 186.76 183.19 254.14 256.70Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 119.08 119.40 119.33 119.73 119.52Tubeside h (W/m2-K) 245.02 246.26 246.05 247.61 246.90Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 245.02 246.26 246.05 247.61 246.90Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 6958 6964 6972 6981 6992Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 6958 6964 6972 6981 6992Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.61 3.61 3.61 3.60 3.60Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 21Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 46 47 48 49 50Tube Pass (--) 3 4 4 4 4Length from tube inlet (mm) 1671.46 1671.46 1503.77 1402.17 1300.57Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -23.79 -23.34 -23.08 -23.01 -22.98Skin temperature (C) -21.94 -21.63 -22.46 -22.45 -22.88MTD (C) 3.4 3.2 1.1 9.799e-1 1.539e-1Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 3.006e-3 3.006e-3 1.199e-3 1.200e-3 1.201e-3Enhanced pressure drop mult (--)Friction loss (kPa) 3.006e-3 3.006e-3 1.199e-3 1.200e-3 1.201e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.722e-2 8.732e-2 8.738e-2 8.739e-2 8.740e-2Average velocity (m/s) 8.722e-2 8.732e-2 8.737e-2 8.739e-2 8.739e-2Area (m2) 0.140 0.140 0.061 0.061 0.061Cumulative area (m2) 3.211 3.351 3.412 3.472 3.533Duty (MegaWatts) 1.247e-4 1.245e-4 1.829e-5 1.644e-5 2.349e-6Cumulative duty (MegaWatts) 0.0026 0.0027 0.0027 0.0027 0.0027Heat flux (W/m2) 891.36 889.59 300.76 270.35 38.62Calculated heat flux (W/m2) 379.41 378.69 128.17 115.22 16.59Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 113.29 119.66 119.99 119.12 116.60Tubeside h (W/m2-K) 249.33 271.10 258.56 255.26 245.64Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 249.33 271.10 258.56 255.26 245.64Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 7016 7054 7075 7080 7083Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 7016 7054 7075 7080 7083Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.60 3.59 3.58 3.58 3.58Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 22Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 51 52 53 54 55Tube Pass (--) 4 4 4 4 4Length from tube inlet (mm) 1198.97 1097.37 995.771 894.171 792.571Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -22.97 -22.97 -22.97 -22.97 -22.97Skin temperature (C) -22.88 -23.25 -23.25 -23.57 -23.57MTD (C) 1.408e-1 -5.08e-1 -5.06e-1 -1.1 -1.1Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 1.201e-3 1.201e-3 1.202e-3 1.202e-3 1.202e-3Enhanced pressure drop mult (--)Friction loss (kPa) 1.201e-3 1.201e-3 1.202e-3 1.202e-3 1.202e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.740e-2 8.740e-2 8.740e-2 8.740e-2 8.740e-2Average velocity (m/s) 8.740e-2 8.740e-2 8.740e-2 8.740e-2 8.740e-2Area (m2) 0.061 0.061 0.061 0.061 0.061Cumulative area (m2) 3.594 3.655 3.716 3.776 3.837Duty (MegaWatts) 2.146e-6 -2.36e-7 -2.35e-7 -4.93e-7 -4.91e-7Cumulative duty (MegaWatts) 0.0027 0.0027 0.0027 0.0027 0.0027Heat flux (W/m2) 35.30 -3.88 -3.86 -8.11 -8.08Calculated heat flux (W/m2) 15.16 -7.76 -7.72 -16.20 -16.13Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 116.18 116.77 116.44 117.07 116.92Tubeside h (W/m2-K) 244.09 246.12 244.92 247.10 246.54Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 244.09 246.12 244.92 247.10 246.54Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 7084 7084 7084 7084 7084Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 7084 7084 7084 7084 7084Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.58 3.58 3.58 3.58 3.58Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 23Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 56 57 58 59 60Tube Pass (--) 4 4 4 4 4Length from tube inlet (mm) 690.971 589.371 487.771 386.171 284.571Mass fraction vapor (--) 0.0000 0.0000 0.0000 0.0000 0.0000Bulk temperature (C) -22.97 -22.98 -22.98 -22.98 -22.99Skin temperature (C) -23.85 -23.85 -24.11 -24.11 -24.38MTD (C) -1.5 -1.5 -2.0 -2.0 -2.5Pressure (kPa) 0.000 0.000 0.000 0.000 0.000Pressure drop (kPa) 1.203e-3 1.203e-3 1.203e-3 1.203e-3 1.204e-3Enhanced pressure drop mult (--)Friction loss (kPa) 1.203e-3 1.203e-3 1.203e-3 1.203e-3 1.204e-3Static head loss (kPa) 0.000 0.000 0.000 0.000 0.000Momentum loss (kPa) 0.000 0.000 0.000 0.000 0.000Maximum velocity (m/s) 8.740e-2 8.740e-2 8.740e-2 8.740e-2 8.740e-2Average velocity (m/s) 8.740e-2 8.740e-2 8.739e-2 8.739e-2 8.739e-2Area (m2) 0.061 0.061 0.061 0.061 0.061Cumulative area (m2) 3.898 3.959 4.020 4.080 4.141Duty (MegaWatts) -7.19e-7 -7.16e-7 -9.32e-7 -9.29e-7 -1.15e-6Cumulative duty (MegaWatts) 0.0027 0.0027 0.0027 0.0027 0.0027Heat flux (W/m2) -11.82 -11.78 -15.32 -15.27 -18.92Calculated heat flux (W/m2) -23.59 -23.51 -30.57 -30.46 -37.73Critical heat flux (W/m2) 0.00 0.00 0.00 0.00 0.00Overall U (W/m2-K) 117.20 117.10 117.33 117.24 117.39Tubeside h (W/m2-K) 247.46 247.08 247.83 247.50 247.94Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 247.46 247.08 247.83 247.50 247.94Sensible vapor h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Condensate film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Vapor phase h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Nucleate boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Conv. boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Film boiling h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Boiling thin film h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Natural convective h (W/m2-K) 0.00 0.00 0.00 0.00 0.00Local Reynolds (--) 7083 7083 7083 7083 7082Vapor Reynolds (--) 0 0 0 0 0Liquid Reynolds (--) 7083 7083 7083 7083 7082Vapor Prandtl (--) 0.00 0.00 0.00 0.00 0.00Liquid Prandtl (--) 3.58 3.58 3.58 3.58 3.58Flow regime param. (--) 0.0000 0.0000 0.0000 0.0000 0.0000Condensate regime (--)Boiling regime (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens LiqBoiling mechanism (--) Sens Liq Sens Liq Sens Liq Sens Liq Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Tubeside Incremental Monitor Page 24Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPoint number (--) 61 62Tube Pass (--) 4 4Length from tube inlet (mm) 116.885 0.000Mass fraction vapor (--) 0.0000 0.0000Bulk temperature (C) -22.99 -23.00Skin temperature (C) -24.35MTD (C) -2.4Pressure (kPa) 0.000 0.000Pressure drop (kPa) 3.011e-3 0.040Enhanced pressure drop mult (--)Friction loss (kPa) 3.011e-3Static head loss (kPa) 0.000Momentum loss (kPa) 0.000Maximum velocity (m/s) 8.739e-2Average velocity (m/s) 8.739e-2Area (m2) 0.140Cumulative area (m2) 4.281Duty (MegaWatts) -2.56e-6Cumulative duty (MegaWatts) 0.0027Heat flux (W/m2) -18.33Calculated heat flux (W/m2) -36.55Critical heat flux (W/m2) 0.00Overall U (W/m2-K) 114.20Tubeside h (W/m2-K) 247.35Enhanced heat transfer mult (--)Sensible liquid h (W/m2-K) 247.35Sensible vapor h (W/m2-K) 0.00Condensate film h (W/m2-K) 0.00Vapor phase h (W/m2-K) 0.00Nucleate boiling h (W/m2-K) 0.00Conv. boiling h (W/m2-K) 0.00Film boiling h (W/m2-K) 0.00Boiling thin film h (W/m2-K) 0.00Natural convective h (W/m2-K) 0.00Local Reynolds (--) 7082 7079Vapor Reynolds (--) 0 0Liquid Reynolds (--) 7082 7079Vapor Prandtl (--) 0.00 0.00Liquid Prandtl (--) 3.58 3.58Flow regime param. (--) 0.0000Condensate regime (--)Boiling regime (--) Sens LiqBoiling mechanism (--) Sens Liq

  • C:\Users\kp\Desktop\HTRI-1.htri

    Vibration Analysis Page 25Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesShellside condition Sens. Liquid (Level 2.2)Axial stress loading (Mpa) 0.000 Added mass factor 1.761Beta 4.000

    Position In The Bundle Inlet Center OutletLength for natural frequency (m) 0.335 0.203 0.335Length/TEMA maximum span (--) 0.220 0.133 0.220Number of spans (--) 8 8 8Tube natural frequency (Hz) 525.0 830.4 524.8 +Shell acoustic frequency (Hz)

    Flow Velocities Inlet Center OutletWindow parallel velocity (m/s) 2.604e-2 2.601e-2 2.600e-2Bundle crossflow velocity (m/s) 1.161e-2 2.669e-2 1.160e-2Bundle/shell velocity (m/s) 1.883e-3 4.327e-3 1.880e-3

    Fluidelastic Instability Check Inlet Center Outlet Log decrement HTRI 0.038 0.038 0.038Critical velocity (m/s) 14.40 39.21 14.39Baffle tip cross velocity ratio (--) 0.001 0.001 0.001Average crossflow velocity ratio (--) 0.001 0.001 0.001

    Acoustic Vibration Check Inlet Center Outlet Vortex shedding ratio (--)Chen number (--)Turbulent buffeting ratio (--)

    Tube Vibration Check Inlet Center Outlet Vortex shedding ratio (--) 0.000 0.000 0.000Turbulent buffeting ratio (--) 0.000 0.001 0.000Parallel flow amplitude (mm) 0.000 0.000 0.000Crossflow amplitude (mm) 0.000 0.000 0.000Turbulent buffeting amplitude (mm) 0.000 0.000 0.000Tube gap (mm) 4.763 4.763 4.763Crossflow RHO-V-SQ (kg/m-s2) 0.17 0.92 0.17

    Bundle Entrance/Exit (analysis at first tube row) Entrance Exit

    Fluidelastic instability ratio (--) 0.001 0.001Vortex shedding ratio (--) 0.000 0.000Crossflow amplitude (mm) 0.00000 0.00000Crossflow velocity (m/s) 1.638e-2 1.635e-2Turbulent buffeting amplitude (mm) 0.000 0.000Tubesheet to inlet/outlet support (mm) None None

    Shell Entrance/Exit Parameters Entrance ExitImpingement plate NoFlow area (m2) 1.670e-3 1.670e-3Velocity (m/s) 7.429e-2 7.418e-2RHO-V-SQ (kg/m-s2) 7.14 7.13Shell type BEM Baffle type Single-Seg.Tube type Plain Baffle layout Perpend.Pitch ratio 1.2500 Tube diameter, (mm) 19.050Layout angle 30 Tube material Carbon steel

    Supports/baffle spaceProgram Messages

    + Frequency ratios are based upon lowest natural or acoustic frequency* Items with asterisk exceed a conservative lower limit for vibration-free design. Review your case using the procedure described in Online Help; You may find that a vibration problem is unlikely.

  • C:\Users\kp\Desktop\HTRI-1.htri

    HEAT EXCHANGER RATING DATA SHEET Page 26 SI Units

    Service of Unit Item No. Type BEM Orientation Horizontal Connected In 1 Parallel 1 SeriesSurf/Unit (Gross/Eff) 4.38 / 4.28 m2 Shell/Unit 1 Surf/Shell (Gross/Eff) 4.38 / 4.28 m2

    PERFORMANCE OF ONE UNITFluid Allocation Shell Side Tube SideFluid Name Brine R404A Fluid Quantity, Total kg/s 0.1604 0.2100 Vapor (In/Out) wt% 0.0 0.0 0.0 0.0 Liquid wt% 100.0 100.0 100.0 100.0Temperature (In/Out) C -20.00 -26.00 -33.00 -23.00Density kg/m3 1293.0 1295.0 1263.9 1233.4Viscosity mN-s/m2 12.000 13.800 0.2704 0.2398Specific Heat kJ/kg-C 2.7196 2.9205 1.2803 1.3046Thermal Conductivity W/m-C 0.5036 0.4966 0.0915 0.0874Critical Pressure kPaInlet Pressure kPaVelocity m/s 2.669e-2 8.702e-2Pressure Drop, Allow/Calc kPa 0.191 0.228Average Film Coefficient W/m2-K 501.74 250.99Fouling Resistance (min) m2-K/W 0.000789 0.000690Heat Exchanged 0.0027 MegaWatts MTD (Corrected) 1.1 C Overdesign -78.96 %Transfer Rate, Service 561.25 W/m2-K Calculated 118.11 W/m2-K Clean 146.16 W/m2-K

    CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)Shell Side Tube Side

    Design Pressure kPaG 1034.21 1034.21Design Temperature CNo Passes per Shell 1 4Flow Direction Downward Upward

    Connections In mm 1 @ 26.645 1 @ 26.645Size & Out mm 1 @ 26.645 1 @ 26.645Rating Liq. Out mm @ @

    Tube No. 40 OD 19.050 mm Thk(Avg) 1.650 mm Length 1.829 m Pitch 23.812 mm Layout 30Tube Type Plain Material CARBON STEEL Pairs seal strips 1Shell ID 203.200 mm Kettle ID mm Passlane Seal Rod No 0Cross Baffle Type PERPEND. SINGLE-SEG. %Cut (Diam) 25.0 Impingement Plate NoneSpacing(c/c) 101.600 mm Inlet 233.771 mm No. of Crosspasses 15Rho-V2-Inlet Nozzle 64.01 kg/m-s2 Shell Entrance 7.14 Shell Exit 7.13 kg/m-s2

    Bundle Entrance 0.35 Bundle Exit 0.35 kg/m-s2Weight/Shell 226.19 Filled with Water 295.76 Bundle 65.80 kgNotes: Thermal Resistance, % Velocities, m/s Flow Fractions

    Shell 23.53 Shellside 2.669e-2 A 0.014Tube 56.92 Tubeside 8.702e-2 B 0.682Fouling 19.20 Crossflow 2.628e-2 C 0.048Metal 0.35 Window 2.639e-2 E 0.257

    F 0.000

    1.829 m

    203.200 mm

  • C:\Users\kp\Desktop\HTRI-1.htri

    HEAT EXCHANGER SPECIFICATION SHEET Page 27 SI Units

    Job No.Customer Reference No.Address Proposal No.Plant Location Date 13-06-15 Rev Service of Unit Item No.Size 203.200 x 1828.98 mm Type BEM Horz. Connected In 1 Parallel 1 SeriesSurf/Unit (Gross/Eff) 4.38 / 4.28 m2 Shell/Unit 1 Surf/Shell (Gross/Eff) 4.38 / 4.28 m2

    PERFORMANCE OF ONE UNITFluid Allocation Shell Side Tube SideFluid Name Brine R404A Fluid Quantity, Total kg/hr 577.471 756.004 Vapor (In/Out) Liquid 577.471 577.471 756.004 756.004 Steam Water NoncondensablesTemperature (In/Out) C -20.00 -26.00 -33.00 -23.00Specific Gravity 1.2936 1.2956 1.2644 1.2340Viscosity mN-s/m2 12.000 13.800 0.2704 0.2398Molecular Weight, VaporMolecular Weight, NoncondensablesSpecific Heat kJ/kg-C 2.7196 2.9205 1.2803 1.3046Thermal Conductivity W/m-C 0.5036 0.4966 0.0915 0.0874Latent Heat kJ/kgInlet Pressure kPaVelocity m/s 2.669e-2 8.702e-2Pressure Drop, Allow/Calc kPa 0.191 0.228Fouling Resistance (min) m2-K/W 0.000789 0.000690Heat Exchanged W 2714.17 MTD (Corrected) 1.1 CTransfer Rate, Service 561.25 W/m2-K Clean 146.16 W/m2-K Actual 118.11 W/m2-K

    CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)Shell Side Tube Side

    Design/Test Pressure kPaG 1034.21 / 1034.21 /Design Temperature CNo Passes per Shell 1 4Corrosion Allowance mm

    Connections In mm 1 @ 26.645 1 @ 26.645Size & Out mm 1 @ 26.645 1 @ 26.645Rating Intermediate @ @

    Tube No. 40 OD 19.050 mm Thk(Avg) 1.650 mm Length 1.829 m Pitch 23.812 mm Layout 30Tube Type Plain Material CARBON STEELShell ID 203.200 mm OD mm Shell CoverChannel or Bonnet Channel CoverTubesheet-Stationary Tubesheet-FloatingFloating Head Cover Impingement Plate NoneBaffles-Cross Type SINGLE-SEG. %Cut (Diam) 25.0 Spacing(c/c) 101.600 Inlet 233.771 mmBaffles-Long Seal Type Supports-Tube U-Bend Type Bypass Seal Arrangement Tube-Tubesheet JointExpansion Joint Type Rho-V2-Inlet Nozzle 64.01 kg/m-s2 Bundle Entrance 0.35 Bundle Exit 0.35 kg/m-s2Gaskets-Shell Side Tube Side -Floating Head Code Requirements TEMA ClassWeight/Shell 226.19 Filled with Water 295.76 Bundle 65.80 kgRemarks:

    Reprinted with Permission (v5 )

    1.829 m

    203.200 mm

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    Properties Profile Monitor Page 28Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPhysical Properties Profile: Hot Shellside (Brine) Reference pressure, (kPa) (P1= 0.000)

    (P) 1 2 3 4 5 6 7 8 9 10Temperature, (C) 1 -20.00 -20.21 -20.41 -20.62 -20.83 -21.03 -21.24 -21.45 -21.65 -21.86Heat duty/flow rate, (kJ/kg) 1 0.0000 0.5637 1.1289 1.6955 2.2636 2.8331 3.4040 3.9763 4.5501 5.1253Weight fraction vapor 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Liquid PropertiesDensity, (kg/m3) 1 1293.00 1293.07 1293.14 1293.21 1293.28 1293.34 1293.41 1293.48 1293.55 1293.62Viscosity, (mN-s/m2) 1 12.0000 12.0566 12.1136 12.1710 12.2287 12.2868 12.3453 12.4042 12.4634 12.5230Thermal conductivity, (W/m-C) 1 0.5036 0.5033 0.5031 0.5028 0.5026 0.5024 0.5021 0.5019 0.5016 0.5014Enthalpy, (kJ/kg) 1 0.0000 -0.5637 -1.1289 -1.6955 -2.2636 -2.8331 -3.4040 -3.9763 -4.5501 -5.1253Specific heat, (kJ/kg-C) 1 2.7196 2.7266 2.7335 2.7404 2.7473 2.7543 2.7612 2.7681 2.7750 2.7820Surface tension, (mN/m) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Critical pressure, (kPa) 1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000Latent heat, (kJ/kg) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000

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    Properties Profile Monitor Page 29Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPhysical Properties Profile: Hot Shellside (Brine) Reference pressure, (kPa) (P1= 0.000)

    (P) 11 12 13 14 15 16 17 18 19 20Temperature, (C) 1 -22.07 -22.27 -22.48 -22.69 -22.90 -23.10 -23.31 -23.52 -23.72 -23.93Heat duty/flow rate, (kJ/kg) 1 5.7020 6.2800 6.8595 7.4405 8.0229 8.6067 9.1919 9.7786 10.3667 10.9563Weight fraction vapor 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Liquid PropertiesDensity, (kg/m3) 1 1293.69 1293.76 1293.83 1293.90 1293.97 1294.03 1294.10 1294.17 1294.24 1294.31Viscosity, (mN-s/m2) 1 12.5830 12.6434 12.7041 12.7653 12.8268 12.8888 12.9512 13.0139 13.0771 13.1407Thermal conductivity, (W/m-C) 1 0.5012 0.5009 0.5007 0.5005 0.5002 0.5000 0.4997 0.4995 0.4993 0.4990Enthalpy, (kJ/kg) 1 -5.7020 -6.2800 -6.8595 -7.4405 -8.0229 -8.6067 -9.1919 -9.7786 -10.367 -10.956Specific heat, (kJ/kg-C) 1 2.7889 2.7958 2.8028 2.8097 2.8166 2.8235 2.8305 2.8374 2.8443 2.8512Surface tension, (mN/m) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Critical pressure, (kPa) 1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000Latent heat, (kJ/kg) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000

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    Properties Profile Monitor Page 30Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPhysical Properties Profile: Hot Shellside (Brine) Reference pressure, (kPa) (P1= 0.000)

    (P) 21 22 23 24 25 26 27 28 29 30Temperature, (C) 1 -24.14 -24.34 -24.55 -24.76 -24.96 -25.17 -25.38 -25.58 -25.79 -26.00Heat duty/flow rate, (kJ/kg) 1 11.5473 12.1397 12.7335 13.3288 13.9255 14.5237 15.1233 15.7243 16.3267 16.9310Weight fraction vapor 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Liquid PropertiesDensity, (kg/m3) 1 1294.38 1294.45 1294.52 1294.59 1294.65 1294.72 1294.79 1294.86 1294.93 1295.00Viscosity, (mN-s/m2) 1 13.2047 13.2691 13.3339 13.3992 13.4649 13.5310 13.5976 13.6646 13.7321 13.8000Thermal conductivity, (W/m-C) 1 0.4988 0.4985 0.4983 0.4981 0.4978 0.4976 0.4974 0.4971 0.4969 0.4966Enthalpy, (kJ/kg) 1 -11.547 -12.140 -12.733 -13.329 -13.926 -14.524 -15.123 -15.724 -16.327 -16.931Specific heat, (kJ/kg-C) 1 2.8582 2.8651 2.8720 2.8789 2.8859 2.8928 2.8997 2.9066 2.9136 2.9205Surface tension, (mN/m) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Critical pressure, (kPa) 1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000Latent heat, (kJ/kg) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000

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    Properties Profile Monitor Page 31Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPhysical Properties Profile: Cold Tubeside (R404A) Reference pressure, (kPa) (P1= 0.000)

    (P) 1 2 3 4 5 6 7 8 9 10Temperature, (C) 1 -23.00 -23.34 -23.69 -24.03 -24.38 -24.72 -25.07 -25.41 -25.76 -26.10Heat duty/flow rate, (kJ/kg) 1 12.9327 12.4827 12.0330 11.5835 11.1344 10.6856 10.2370 9.7887 9.3407 8.8931Weight fraction vapor 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Liquid PropertiesDensity, (kg/m3) 1 1233.42 1234.47 1235.52 1236.57 1237.62 1238.67 1239.72 1240.77 1241.82 1242.87Viscosity, (mN-s/m2) 1 0.2398 0.2407 0.2417 0.2427 0.2436 0.2446 0.2456 0.2466 0.2476 0.2486Thermal conductivity, (W/m-C) 1 0.0874 0.0875 0.0877 0.0878 0.0880 0.0881 0.0882 0.0884 0.0885 0.0887Enthalpy, (kJ/kg) 1 0.0000 -0.4500 -0.8997 -1.3491 -1.7983 -2.2471 -2.6957 -3.1440 -3.5919 -4.0396Specific heat, (kJ/kg-C) 1 1.3046 1.3038 1.3029 1.3021 1.3012 1.3004 1.2996 1.2987 1.2979 1.2971Surface tension, (mN/m) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Critical pressure, (kPa) 1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000Latent heat, (kJ/kg) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000

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    Properties Profile Monitor Page 32Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPhysical Properties Profile: Cold Tubeside (R404A) Reference pressure, (kPa) (P1= 0.000)

    (P) 11 12 13 14 15 16 17 18 19 20Temperature, (C) 1 -26.45 -26.79 -27.14 -27.48 -27.83 -28.17 -28.52 -28.86 -29.21 -29.55Heat duty/flow rate, (kJ/kg) 1 8.4456 7.9985 7.5517 7.1052 6.6589 6.2130 5.7673 5.3219 4.8768 4.4320Weight fraction vapor 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Liquid PropertiesDensity, (kg/m3) 1 1243.92 1244.97 1246.02 1247.07 1248.12 1249.16 1250.21 1251.26 1252.31 1253.36Viscosity, (mN-s/m2) 1 0.2496 0.2507 0.2517 0.2527 0.2538 0.2548 0.2559 0.2569 0.2580 0.2591Thermal conductivity, (W/m-C) 1 0.0888 0.0890 0.0891 0.0892 0.0894 0.0895 0.0897 0.0898 0.0900 0.0901Enthalpy, (kJ/kg) 1 -4.4870 -4.9341 -5.3810 -5.8275 -6.2738 -6.7197 -7.1654 -7.6108 -8.0559 -8.5007Specific heat, (kJ/kg-C) 1 1.2962 1.2954 1.2946 1.2937 1.2929 1.2920 1.2912 1.2904 1.2895 1.2887Surface tension, (mN/m) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Critical pressure, (kPa) 1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000Latent heat, (kJ/kg) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000

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    Properties Profile Monitor Page 33Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesPhysical Properties Profile: Cold Tubeside (R404A) Reference pressure, (kPa) (P1= 0.000)

    (P) 21 22 23 24 25 26 27 28 29 30Temperature, (C) 1 -29.90 -30.24 -30.59 -30.93 -31.27 -31.62 -31.96 -32.31 -32.65 -33.00Heat duty/flow rate, (kJ/kg) 1 3.9875 3.5433 3.0993 2.6557 2.2123 1.7692 1.3265 0.8840 0.4418 0.0000Weight fraction vapor 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Liquid PropertiesDensity, (kg/m3) 1 1254.41 1255.46 1256.51 1257.56 1258.61 1259.66 1260.71 1261.76 1262.81 1263.86Viscosity, (mN-s/m2) 1 0.2602 0.2613 0.2624 0.2635 0.2646 0.2658 0.2669 0.2680 0.2692 0.2704Thermal conductivity, (W/m-C) 1 0.0903 0.0904 0.0905 0.0907 0.0908 0.0910 0.0911 0.0913 0.0914 0.0915Enthalpy, (kJ/kg) 1 -8.9452 -9.3894 -9.8333 -10.277 -10.720 -11.163 -11.606 -12.049 -12.491 -12.933Specific heat, (kJ/kg-C) 1 1.2879 1.2870 1.2862 1.2853 1.2845 1.2837 1.2828 1.2820 1.2812 1.2803Surface tension, (mN/m) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Critical pressure, (kPa) 1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000Latent heat, (kJ/kg) 1 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000

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    Stream Properties Page 34Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesHot Shellside Fluid Inlet OutletFluid name BrineTemperature (C) -20.00 -26.00Pressure (kPa) 0.000 0.000Weight fraction vapor (--) 0.0000 0.0000

    Vapor PropertiesDensity (kg/m3) -- --Viscosity (mN-s/m2) -- --Conductivity (W/m-C) -- --Heat capacity (kJ/kg-C) -- --Molecular weight (--) -- --

    Liquid PropertiesDensity (kg/m3) 1293.00 1295.00Viscosity (mN-s/m2) 12.0000 13.8000Conductivity (W/m-C) 0.5036 0.4966Heat capacity (kJ/kg-C) 2.7196 2.9205Molecular weight (--) 0 0Latent heat (kJ/kg) -- --Surface tension (mN/m) 0.0000 0.0000

    Molar Composition Vapor Liquid K-Value Vapor Liquid K-Value1 Brine -- -- -- -- -- --

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    Stream Properties Page 35Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesCold Tubeside Fluid Inlet OutletFluid name R404ATemperature (C) -33.00 -23.00Pressure (kPa) 0.000 0.000Weight fraction vapor (--) 0.0000 0.0000

    Vapor PropertiesDensity (kg/m3) -- --Viscosity (mN-s/m2) -- --Conductivity (W/m-C) -- --Heat capacity (kJ/kg-C) -- --Molecular weight (--) -- --

    Liquid PropertiesDensity (kg/m3) 1263.86 1233.42Viscosity (mN-s/m2) 0.2704 0.2398Conductivity (W/m-C) 0.0915 0.0874Heat capacity (kJ/kg-C) 1.2803 1.3046Molecular weight (--) 0 0Latent heat (kJ/kg) -- --Surface tension (mN/m) 0.0000 0.0000

    Molar Composition Vapor Liquid K-Value Vapor Liquid K-Value1 -- -- -- -- -- --

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    Input Reprint Page 36Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesShell DataService type Generic Shell and TubeTEMA type BEMRun mode RatingHot fluid location ShellsideNumber of shells in series 1Number of shells in parallel 1Shell inside diameter 203.200 mmFlow in 1st tubepass CountercurrentTrain flow direction Countercurrent

    Reboiler DataReboiler type No piping specifiedInlet pressure location Inlet nozzle

    Tube DataTube type PlainTube outside diameter 19.050 mmTube wall thickness 1.650 mmTube pitch 23.813 mmTube pitch ratio 1.250Tubepasses per shell 4Tube pattern 30 degreesNumber of tubes per shell 40Tube count method RigorousTube length 1.829 mTube material Carbon steel

    Tubepass Arrangement DataForce symmetric layout NoForce cleaning lanes NoTubes to remove for tie rods Calculated

    Baffle DataBaffle type Single segmentalBaffle orientation Program setsBaffle cut percent 25 % shell IDCentral baffle spacing 101.600 mmVariable baffle spacing NoWindow cut from baffles No

    Clearance DataNumber of seal strip pairs CalculatedBaffle clearance type TEMABlock A stream NoBlock E stream NoBlock F stream NoNumber of passlane seal rods Calculated

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    Input Reprint Page 37Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesNozzle DataNumber of shellside inlet nozzles 1Number of shellside outlet nozzles 1Number of tubeside inlet nozzles 1Number of tubeside outlet nozzles 1Radial position on shell inlet nozzle Program decidesLongitudinal position on shell of inlet nozzle At rear headRadial position on shell outlet nozzle Program decidesTubeside entry type RadialTubeside inlet position Front headTubeside exit type Same as inletFront head location Left

    Impingement DataImpingement device present If required by TEMAImpingement type Circular plate

    Optional Geometry DataSmall exchanger NoTubesheet type SingleShell expansion joint NoFloating head support type NoneInsulated longitudinal baffle No

    Process Conditions Data Hot Fluid Cold FluidPhase condition Sensible liquid Sensible liquidFlow rate 0.2100 kg/sInlet vapor fraction 0 0Outlet vapor fraction 0 0Inlet temperature -20.00 -33.00 COutlet temperature -26.00 -23.00 CDuty multiplier 1

    Process Fouling Data Hot Fluid Cold FluidFouling resistance 7.900e-4 6.900e-4 m2-K/W

    Hot Fluid Property DataFluid name BrinePhysical property method Component by component propertiesHeat release method Program calculatedFlash type IntegralQuantity units MolesTemperature interpolation option ProgramNumber of components 1

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    Input Reprint Page 38Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesHot Fluid Component DataComponent number 1Component name BrineComp. bank name Component bank NoneComponent phase LiquidLiquid Properties Reference temperature, C -20.00 -26.00 Density, kg/m3 1293.00 1295.00 Viscosity, mN-s/m2 12.0000 13.8000 Thermal conductivity, W/m-C 0.5034 0.4965 Heat capacity, kJ/kg-C 2.7196 2.9204

    Cold Fluid Property DataFluid name R404APhysical property method Component by component propertiesHeat release method Program calculatedFlash type IntegralQuantity units MolesTemperature interpolation option ProgramNumber of components 1

    Cold Fluid Component DataComponent number 1Comp. bank name Component bank NoneComponent phase MixedLiquid Properties Reference temperature, C -33.00 -23.00 Density, kg/m3 1263.86 1233.42 Viscosity, mN-s/m2 0.2704 0.2398 Thermal conductivity, W/m-C 0.0915 0.0874 Heat capacity, kJ/kg-C 1.2803 1.3046

    Control Methods DataShellside friction factor method CommercialTubeside friction factor method CommercialPure longitudinal flow NoPure component condensation NoCondensing correlation HTRI ProrationMole fraction inerts 0Momentum exclusion 0 %Pure component boiling NoCheck film boiling YesNucleate boiling method Physical property/theoretical boiling rangeComponent boiling method Nucleate and convective

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    Input Reprint Page 39Released to the following HTRI Member Company: SYNERGY KALPAN

    Xist E Ver. 5.00 13-06-15 14:10 SN: Friendsl SI Units

    Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental BafflesControl Safety DataHot fluid/shellside film coefficient multiplier 1Hot fluid/shellside friction factor multiplier 1Cold fluid/tubeside film coefficient multiplier 1Cold fluid/tubeside friction factor multiplier 1Cold fluid fraction of critical flux for film boiling 1

    Control User-Defined Methods DataAdd non-nucleate boiling Yes

    Control Vibration DataDamping factor method HTRI MethodInclude inlet vibration support NoInclude outlet vibration support No